1. No category

Basics of Thermodynamics
Some of the material covered here is also covered in the chapter/topic on:
Equilibrium
MATERIALS SCIENCE
Part of
& A Learner’s Guide
ENGINEERING
AN INTRODUCTORY E-BOOK
Anandh Subramaniam & Kantesh Balani
Materials Science and Engineering (MSE)
Indian Institute of Technology, Kanpur- 208016
Email: [email protected], URL: home.iitk.ac.in/~anandh
http://home.iitk.ac.in/~anandh/E-book.htm
Reading
Four Laws that Drive the Universe
Peter Atkins*
Oxford University Press, Oxford, 2007
Physical Chemistry
Ira N Levine
Tata McGraw Hill Education Pvt. Ltd., New York (2002).
*It is impossible for me to write better than Atkins- his lucid (& humorous) writing style is truly impressive- paraphrasing may lead to loss of
the beauty of his statements- hence, some parts are quoted directly from his works.
Thermodynamics versus Kinetics
 Thermodynamics deals with stability of systems. It tells us ‘what should
happen?’. ‘Will it actually happen(?)’ is not the domain of thermodynamics and
falls under the realm of kinetics.
 At –5C at 1 atm pressure, ice is more stable then water. Suppose we cool water
to –5C. “Will this water freeze?” (& “how long will it take for it to freeze?”) is
(are) not question(s) addressed by thermodynamics.
 Systems can remain in metastable state for a ‘long-time’.
 Window pane glass is metastable– but it may take geological time scales for it
to crystallize!
 At room temperature and atmospheric pressure, graphite is more stable then
diamond– but we may not lose the glitter of diamond practically forever!
* The term metastable is defined in the chapter on equilibrium.
Thermodynamics (TD): perhaps the most basic science
 One branch of knowledge that all engineers and scientists must have a grasp of
(to some extent or the other!) is thermodynamics.
 In some sense thermodynamics is perhaps the ‘most abstract subject’ and a
student can often find it very confusing if not ‘motivated’ strongly enough.
 Thermodynamics can be considered as a ‘system level’ science- i.e. it deals with
descriptions of the whole system and not with interactions (say) at individual
particles level.
 I.e. it deals with quantities (like T,P) averaged over a large collection of entities
(like molecules, atoms)*.
 This implies that questions like: “What is the temperature or entropy of an
atom?”; do not make sense in the context of thermodynamics (at lease in the usual way!).
 TD puts before us some fundamental laws which are universal** in nature (and
hence applicable to fields across disciplines).
* Thermodynamics deals with spatio-temporally averaged quantities.
** they apply to the universe a whole as well!
The language of TD
 To understand the laws of thermodynamics and how they work, first we need to get the
terminology right. Some of the terms may look familiar (as they are used in everyday
language as well)- but their meanings are more ‘technical’ and ‘precise’, when used in TD
and hence we should not use them ‘casually’.
 System is region where we focus our attention (Au block in figure).
 Surrounding is the rest of the universe (the water bath at constant ‘temperature’).
 Universe = System + Surrounding
 More practically, we can consider the ‘Surrounding’ as the immediate neighbourhood of
the system (the part of the universe at large, with which the system ‘effectively’ interacts).
In this scheme of things we can visualize: a system, the surrounding and the universe at
large.
In TD we usually we do not worry
about the universe at large!
Open, closed and isolated systems
 To a thermodynamic system two ‘things’ may be added/removed:
 energy (heat, work)  matter.
 An open system is one to which you can add/remove matter (e.g. a open beaker to which
we can add water). When you add matter- you also end up adding heat (which is contained
in that matter).
 A system to which you cannot add matter is called closed.
Though you cannot add/remove matter to a closed system, you can still add/remove heat
(you can cool a closed water bottle in fridge).
 A system to which neither matter nor heat can be added/removed is called isolated.
A closed vacuum ‘thermos’ flask can be considered as isolated.
Type of boundary
Interactions
Open
All interactions possible
Closed
Matter cannot enter or leave
Semi-permeable
Only certain species can enter or leave
Insulated
Heat cannot enter or leave
Rigid
Mechanical work cannot be done*
Isolated
No interactions are possible**
* By or on the system
** Mass, Heat or Work
Mass
Interactions possible
Work
Heat
 Matter is easy to understand and includes atoms, ions, electrons, etc.
 Energy may be transferred (‘added’) to the system as heat, electromagnetic radiation etc.
 In TD the two modes of transfer of energy to the system considered are Heat and Work.
 Heat and work are modes of transfer of energy and not ‘energy’ itself.
 Once inside the system, the part which came via work and the part which came via
heat, cannot be distinguished. More sooner on this!
 Matter when added to a system brings along with it some energy. The ‘energy density’
(energy per unit mass or energy per unit volume) in the incoming matter may be higher or lower than the
matter already present in the system.
Processes in TD
We will deal with some of them in detail later on
 Here is a brief listing of a few kinds of processes, which we will encounter in TD:
 Isothermal process → the process takes place at constant temperature
(e.g. freezing of water to ice at –10C)
 Isobaric → constant pressure
(e.g. heating of water in open air→ under atmospheric pressure)
 Isochoric → constant volume
(e.g. heating of gas in a sealed metal container)
 Reversible process → the system is close to equilibrium at all times (and infinitesimal
alteration of the conditions can restore the universe (system + surrounding) to the original
state.
 Cyclic process → the final and initial state are the same. However, q and w need not be
zero.
 Adiabatic process → dq is zero during the process (no heat is added/removed to/from the
system)
 A combination of the above are also possible: e.g. ‘reversible adiabatic process’.
Temperature
 Though we all have a feel for temperature (‘like when we are feeling hot’); in the context
of TD temperature is technical term with ‘deep meaning’.
 As we know (from a commons sense perspective) that temperature is a measure of the ‘intensity of
heat’. ‘Heat flows’ (energy is transferred as heat) from a body at higher temperature to one at lower
temperature. (Like pressure is a measure of the intensity of ‘force applied by matter’→
matter (for now a fluid) flows from region of higher pressure to lower pressure).
 That implies (to reiterate the obvious!) if I connect two bodies (A)-one weighing 100kg at 10C
and the other (B) weighing 1 kg at 500C, then the ‘heat will flow’ from the hotter body to
the colder body (i.e. the weight or volume of the body does not matter).
 But, temperature comes in two important ‘technical’ contexts in TD:
1 it is a measure of the average kinetic energy (or velocity) of the constituent entities (say molecules)
2 it is the parameter which determines the distribution of species (say molecules) across
various energy states available.
A
10C
Heat flow
direction
B
500C
Temperature as a parameter determining the distribution of species across energy levels
 Let us consider various energy levels available for molecules in a system to be promoted to.
 At low temperatures the lower energy levels are expected to be populated more, as compared to
higher energy levels. As we heat the system, more and more molecules will be promoted to
higher energy levels.
 The distribution of molecules across these energy levels is given by:
Pressure
 Pressure* is force per unit area (usually exerted by a fluid on a wall**).
 It is the momentum transferred (say on a flat wall by molecules of a gas) per unit area, per unit time. (In
the case of gas molecules it is the average momentum transferred per unit area per unit time on to the flat wall).
 P = momentum transferred/area/time.
Wall of a container
 Pressure is related to momentum, while temperature is related to kinetic energy.
‘Crude schematic’
of particles
impinging on a
wall.
* ‘Normal’ pressure is also referred to as hydrostatic pressure.
** Other agents causing pressure could be radiation, macroscopic objects impinging on a wall, etc.
Heat and Work
 Work (W) in mechanics is displacement (d) against a resisting force (F). W = F  d
 Work has units of energy (Joule, J).
 Work can be expansion work (PV), electrical work, magnetic work etc. (many sets of
stimuli and their responses).
 Heat as used in TD is a tricky term (yes, it is a very technical term as used in TD).
 The transfer of energy as a result of a temperature difference is called heat.
 “In TD heat is NOT an entity or even a form of energy; heat is a mode of transfer of
energy” [1].
 “Heat is the transfer of energy by virtue of a temperature difference” [1].
 “Heat is the name of a process, not the name of an entity” [1].
 “Bodies contain internal energy (U) and not heat” [2].
 The ‘flow’ of energy down a temperature gradient can be treated mathematically by
considering heat as a mass-less fluid [1] → this does not make heat a fluid!
Expansion work
To give an example (inspired by [1]):
assume that you start a rumour that there is ‘lot of’ gold under the class room floor. This rumour ‘may’ spread when persons talk to each other.
The ‘spread of rumor’ with time may be treated mathematically by equations, which have a form similar to the diffusion equations (or heat
transfer equations). This does not make ‘rumour’ a fluid!
[1] Four Laws that Drive the Universe, Peter Atkins, Oxford University Press, Oxford, 2007. [2] Physical Chemistry, Ira N Levine, Tata McGraw Hill Education Pvt. Ltd., New York (2002).
 Work is coordinated flow of matter.
 Lowering of a weight can do work
 Motion of piston can do work
 Flow of electrons in conductor can do work.
 Heat involves random motion of matter (or the constituent entities of matter).
 Like gas molecules in a gas cylinder
 Water molecules in a cup of water
 Atoms vibrating in a block of Cu.
 Energy may enter the system as heat or work.
 Once inside the system:
 it does not matter how the energy entered the system* (i.e. work and heat are terms
associated with the surrounding and once inside the system there is no ‘memory’ of how
the input was received and
 the energy is stored as potential energy (PE) and kinetic energy (KE).
 This energy can be withdrawn as work or heat from the system.
* As Aktins put it: “money may enter a back as cheque or cash but once inside the bank there is no difference”.
Reversible process
‘Reversible’ is a technical term (like many others) in the context of TD.
 A reversible process is one where an infinitesimal change in the conditions of the
surroundings leads to a ‘reversal’ of the process. (The system is very close to equilibrium
and infinitesimal changes can restore the system and surroundings to the original state).
 If a block of material (at T) is in contact with surrounding at (TT), then ‘heat will flow’
into the surrounding. Now if the temperature of the surrounding is increased to (T+T),
then the direction of heat flow will be reversed.
 If a block of material (at 40C) is contact with surrounding at 80C then the ‘heat transfer’
with takes place is not reversible.
 Though the above example uses temperature differences to illustrate the point, the
situation with other stimuli like pressure (differences) is also identical.
 Consider a piston with gas in it a pressure ‘P’. If the external pressure is (P+P), then the
gas (in the piston) will be compressed (slightly). The reverse process will occur if the
external (surrounding pressure is slightly lower).
 Maximum work will be done if the compression (or expansion) is carried out in a
reversible manner.
Reversible process
Heat flow
direction
Heat flow
direction
T
TT
NOT a Reversible process
Heat flow
direction
T
T+T
40C
80C
How to visualize a ‘reversible’ equivalent to a ‘irreversible’ processes?
 Let us keep one example in mind as to how we can (sometimes) construct a ‘reversible’
equivalent to a ‘irreversible’ processes.
 Let us consider the example of the freezing of ‘undercooled water’* at –5C (at 1 atm
pressure). This freezing of undercooled water is irreversible (P1 below).
 We can visualize this process as taking place in three reversible steps  hence making the
entire process reversible (P2 below).
P1
Water at –5C
Irreversible
Water at –0C
P2
Heat
Water at –5C
Ice at –5C
Ice at –0C
Reversible
Cool
Ice at –5C
* ‘Undercooled’ implies that the water is held in the liquid state below the bulk freezing point! How is this possible?→ read chapter on phase
transformations
Reversible P-V work on a closed system
 In a closed system (piston in the example figure below), if infinitesimal pressure increase
causes the volume to decrease by V, then the work done on the system is:
 The system is close to equilibrium during the whole process
thus making the process reversible.
dwreversible   PdV
 As V is negative, while the work done is positive (work done on the system is positive,
work done by the system is negative).
If the piston moves outward under influence of P (i.e. ‘P’ and V are in opposite directions,
then work done is negative.
1
P
2
 ‘Ultimately’, all forms of energy will be converted to heat!!
 One nice example given by Atkins: consider a current through a heating wire of a resistor.
There is a net flow of electrons down the wire (in the direction of the potential gradient)
 i.e. work is being done.
Now the electron collisions with various scattering centres leading to heating of the wire
 i.e. work has been converted into heat.
State functions in TD
 A property which depends only on the current state of the system (as defined by T, P, V
etc.) is called a state function. This does not depend on the path used to reach a particular
state.
 Analogy: one is climbing a hill- the potential energy of the person is measured by the
height of his CG from ‘say’ the ground level. If the person is at a height of ‘h’ (at point P),
then his potential energy will be mgh, irrespective of the path used by the person to reach
the height (paths C1 & C2 will give the same increase in potential energy of mgh- in
figure below).
 In TD this state function is the internal energy (U or E). (Every state of the system can be ascribed to a unique U).
 Hence, the work needed to move a system from a state of lower internal energy (=UL) to a
state of higher internal energy (UH) is (UH)  (UL). W = (UH)  (UL)
 The internal energy of an isolated system (which exchages neither heat nor mass) is
constant  this is one formulation of the first law of TD.
 A process for which the final and initial states are same is called a cyclic process. For a
cyclic process change in a state function is zero.
E.g. U(cyclic process) = 0.
Spontaneous and Driven processes
 A spontaneous process is one which occurs ‘naturally’, ‘down-hill’ in energy*. I.e. the
process does not require input of work in any form to take place.
 Melting of ice at 50C is a spontaneous process.
 A driven process is one which wherein an external agent takes the system uphill in energy
(usually by doing work on the system).
 Freezing of water at 50C is a driven process (you need a refrigerator, wherein electric
current does work on the system).
 Later on we will note that the entropy of the universe will increase during a spontaneous
change. (I.e. entropy can be used as a single parameter for characterizing spontaneity).
Spontaneous process
(Click to see)
* The kind of ‘energy’ we are talking about depends on the conditions. As in the topic on Equilibrium, at constant temperature and pressure the
relevant TD energy is Gibbs free energy.
Heat Capacity
 Heat capacity is the amount of heat (measured in Joules or Calories) needed to raise an
unit amount of substance (measured in grams or moles) by an unit in temperature
(measured in C or K).
 This ‘heating’ (addition of energy) can be carried out at constant volume or constant
pressure. At constant pressure, some of the heat supplied goes into doing work of
expansion and less is available with the system (to raise it temperature).
 Heat capacity at constant Volume (CV):
 E 
C

V


It is the slope of the plot of internal energy with temperature.
 T V
 Heat capacity at constant Pressure (CP):
 H 
It is the slope of the plot of enthalpy with temperature.
CP  

 T  P
 Units: Joules/Kelvin/mole, J/K/mole, J/C/mole, J/C/g.
 Heat capacity is an extensive property (depends on ‘amount of matter’)
 If a substance has higher heat capacity, then more heat has to be added to raise its
temperature. Water with a high heat capacity (of *****) heats up slowly as compared to
air (with a heat capacity, CP = 29.07J/K/mole)  this implies that oceans will heat up slowly as
compared to the atomosphere.
 As T0K, the heat capacity tends to zero. I.e near 0 Kelvin very little heat is required to
raise the temperature of a sample. (This automatically implies that very little heat has to
added to raise the temperature of a material close to 0K.
This is of course bad news for cooling to very low temperatures small leakages of heat will lead to drastic increase in temperature).
The Laws of Thermodynamics The First Law
 The internal energy of an isolated system is constant.
 A closed system may exchange energy as heat or work. Let us consider a close system at
rest without external fields.
 There exists a state function U such that for any process in a closed system:
U = q + w [1]
 q → heat flow in to the system
 w → work done on the system (work done by the system is negative of above- this is just ‘one’ sign convention)
q & w are not state functions → i.e. they depend on the path of a process.
 U is the internal energy. Being a state function for a process U depends only of the final
and initial state of the system. U = Ufinal – Uinitial. In contrast to U, q & w are NOT state
functions (i.e. depend on the path followed).
 For an infinitesimal process eq. [1] can be written as: dU = dq + dw
 The change in U of the surrounding will be opposite in sign, such that:
Usystem + Usurrounding = 0
 Actually, it should be E above and not U {however, in many cases K and V are zero
(e.g. a system at rest considered above) and the above is valid- as discussed elsewhere}.

It is to be noted that in ‘w’ work done by one part of the system on another part is not included.
The Second Law
The second law comes in many equivalent forms
 It is impossible to build a cyclic machine that converts heat into work with 100% efficiency
 Kelvin’s statement of the second law.
 Another way of viewing the same:
it is impossible to construct a cyclic machine* that completely (with 100% efficiency)
converts heat, which is energy of random molecular motion, to mechanical work, which is
ordered motion.
 The unavailable work is due to the role of Entropy in the process.
Heat reservoir
Heat q

Cyclic engine
Not possible
100%
Heat reservoir
Heat q
Work (w)
Cyclic engine
Heat q’
Cold Reservoir
Work (w)
* These ‘engines’ which use heat and try to produce work are called heat engines.

Kelvin’s
statement of the
second law
Another statement of the second law → the Clausius statement
 Heat does not ‘flow*’ from a colder body to a hotter body, without an concomitant change
outside of the two bodies Clausius’s statement of the second law.(a)
 This automatically implies that the spontaneous direction of the ‘flow of heat*’ is from a
hotter body to a colder body.(b)
 The Kelvin’s and Clausius’s statements of the second law are equivalent. I.e. if we violate
Kelvin’s statement, then we will automatically violate the Clausius’s statement of the
second law (and vice-versa).
* Used here in the ‘common usage sense’.
(b) is obvious, but not (a) → though they represent the same fact.
A combined (Kelvin + Clausius) statement of the II Law
 The entropy of the universe will increase during any spontaneous change.
The efficiency of a heat engine
 The efficiency of a heat engine is the amount of work output divided by the amount of heat
input.
 This efficiency depends only on the ratio of the temperature of the sink to the temperature
of the source. The maximum efficiency achievable is given by the formula below.
 This is surprising as:
 there is no mention of the medium of the system (or its properties),
 the formula has only temperatures and
 the temperature of the sink seems to play a major role (as the presence of the sink is
usually not intentional or obvious→ in a steam engine sink is the air around the engine and
source is the hot steam).
Important message Sink (characterized by its temperature) is as important as the source.
 To increase the maximum possible efficiency of a heat engine, either the temperature of the
source has to be increased on the temperature of the sink has to be decreased.
heat engine 
woutput
qinput
 Tsink 

T
 source 
max
heat
engine  1  
Clausius statement of the second law
 Heat cannot spontaneously flow from a cold (low temperature) body to a hot body.
 To make heat flow from a cold body to a hot body, there must be accompanying change
elsewhere (work has to be done to achieve this).
The Third Law
 For substances in internal equilibrium, undergoing an isothermal process, the entropy
change goes to zero as T (in K) goes to zero.
lim S  0
T 0
 The law is valid for pure substances and mixtures.
 Close to Zero Kelvin, the molecular motions have to be treated using quantum mechanics
→ still it is found that quantum ideal gases obey the third law.
Ideal and Perfect Gases
 To understand the basics often we rely on simple ‘test-bed’ systems.
 In TD one such system is the ideal gas. In an ideal gas the molecules do not interact with
each other (Noble gases come close to this at normal temperatures).
An ideal gas obeys the equation of state:
PV  nRT
 As the molecules of a ideal gas do not interact with each other, the internal energy of the
system is expected to be ‘NOT dependent’ on the volume of the system.
I.e.:
U



 0
 V T
 A gas which obeys both the above equations is called a perfect gas.
 Internal energy (a state function) is normally a function of T & V: U = U(T,V).
 For a perfect gas: U = U(T) only.
Humorous look at
the three laws
 The first law says: “you cannot win”.
 The second law says: “you can at best break even- that too at zero Kelvin”.
 Third law says: “zero Kelvin is unattainable”.
What happens when we mix two elements (say Ag and Au→ two crystals)?
 When we mix two (or for that matter more) elements (A & B), the stable phase will be that
with the lowest G. There are three options here (as we have seen in Chapter 4a):
1 Phase separation → A & B do not want to talk to each other
2 Formation of solid solution → A & B do not care about their environment
3 Compound formation → A & B prefer each other’s environment as compared to their own environment
 In a compound the each one of the components are fixed to their sub-lattices and hence the
configurational entropy of the compound is zero. This is true in the case of a complete phase
separation as well (i.e. the configurational entropy is zero).
 The solid solution is also called a disordered solid solution, in which case each component
is randomly occupies a lattice point without any preference. In practice, there might be
some tendency for ‘ordering’ (i.e. compound formation) or ‘clustering’ (phase separation)
and in that case the ‘random configuration’ assumption will be violated.
 The Gibbs free energy change on mixing (for now we visualize mixing– soon we will see if
they actually mix!) is:
Gmix = Gmixed state – Gunmixed state = Hmix – T Smix. H = H
–H
.
mix
mixed state
unmixed
 Hence, if we know two numbers (Hmix, Smix) our job is done!
 The game-plan is to find these numbers (especially, Hmix).
 Various models are used for this purpose and that can be quite confusing!
 Each one of these models come with their own baggage of assumptions (& hence approximations).
 The simplest model of mixing is the formation of the ideal solution. In an ideal solution AB bonds are energetically no different from the A-A or B-B bonds.
This implies that (Hmix)ideal solution = 0.
 If (Hmix)ideal solution  0, which usually happens in practice (i.e. usually the mixing process is
endothermic or exothermic), then we need a more ‘realistic’ computation of Hmix. One of
the popular models is the regular solution model (which is based on the quasi-chemical
approach).
 In real alloys the following factors come into the picture, which can lead to substantial
deviation from the some of the models considered: (i) ordering (if Hmix is very negative),
(ii) clustering (leading to deviation from the random configuration model, (iii) strain in the
lattice due to size difference between the atoms (the quasi-chemical model will
underestimate the change in internal energy on mixing), (iv) substantial size difference
leading to the formation of a interstitial solid solution.
Ideal solution
 Gmix ideal solution  T .Smix
Smix   R( X A ln X A  X B ln X B )
 Gmix ideal solution  RT ( X A ln X A  X B ln X B )
Gmix →
0
A
Increasing T
XB →
B
Regular solution model (quasi-chemical approach)
No change in volume
before and after mixing
 The regular solution model makes the following assumptions:
A + B = AB
(i) the enthalpy of mixing is only due to nearest neighbour atoms,
(ii) volume of A and B (per mole) is the same and there is no volume change due to the
mixing process (interatomic distances and bond energies are independent of the
composition),
(iii) point (ii) above also implies that there is no strain in the lattice.
If no. of A-A bonds (per mole) is NAA, the no. of B-B bonds is NBB and the no. of A-B bonds is
NAB and the corresponding bond energies (per bond) are given by EAA, EBB & EAB the internal
energy of the solution is given by (Esolution): Esolution  N AA EAA  N BB EBB  N AB EAB
The change in internal energy on mixing (noting that since there is no change in volume, E =
H): H mix  N AB E Where E  E  1 ( E  E )
AB
2
AA
BB
Three scenarios are possible regarding the sign of E
E<0 → Hmix negative
Sign of E
AB bonds are preferred over AA or BB bonds
E= 0 → Hmix is zero Ideal solution (no difference between AA, AB or BB bonds
E>0 → Hmix is positive AB bonds less preferred over AA or BB bonds
Let us consider the scenarios a little further
If E= 0 → Hmix is zero Ideal solution (no difference between AA, AB or BB bonds
For an ideal solution it can be shown that: N AB  z N0 X A X B
N0 → Avogadro’s No.
z → No. of bonds per atom
If E is not too negative or E is not too positive
The equation in the case of the ideal solution for NAB can still be used as
an approximation N AB  z N0 X A X B
This implies: H mix  z N0 X A X B E   X A X B
H mix   X A X B
  z N0 E
E  EAB  12 ( EAA  EBB )
 Gmix regular solution   X A X B  RT ( X A ln X A  X B ln X B )
H mix
T Smix
This implies that for regular solutions  is the key parameter determining the behaviour of the
regular solution ( in turn depends on E, which is ‘some’ measure of the relative values of AA
and AB bond energies).
The effect of  (& T)
High T
Could be –T or ‘nothing’
Low T
Could be H, S or G
<0
>0
We will
understand
these figures
in the
coming
slides
Understanding the G- composition curves: General aspects
The  parameter determines
the sign of the Hmix
 is obviously zero for
pure (unmixed) components
As mixing leads to an increase in
entropy and T is always positive
(in K) –TSmix term is always
negative
The Gmix is determined just by the
addition of the Hmix & –TSmix for
each composition
The Smix term only depends on
the composition for a random
solid solution
<0
Hsolution < Hpure components
High T
 As Hmix & –TSmix are both
negative Gmix is always negative.
 Gmix gets more negative with
increasing T due to the –TSmix.
Low T
 The phase diagram of such a system will show
complete solubility at high T and phase
separation for a range of compositions (in the
middle) at low T.
Hsolution > Hpure components
High T
Hmix and –TSmix oppose each
other at high ‘enough’ T, –TSmix
wins at all compositions and Gmix
is always negative
At ‘low’ T, Hmix wins over –TSmix
for some compositions (in the
‘middle’) and Gmix turns positive for
this range of compositions.
Low T
Except at absolute zero (T), Gmix
always decreases on the addition of a
small amount of solute (even if Hmix
gets ‘very’ positive).
>0